U.S. patent number 3,787,038 [Application Number 05/304,307] was granted by the patent office on 1974-01-22 for reformer for firing reverberatory furnace and method of operating said reformer.
Invention is credited to Alexandr Kornilovich Ivanov, Evgeny Mikhailovich Kondratiev, Konstantin Ivanovich Makarov, Grigory Isaevich Moiseevich, Igor Ivanovich Osmaga, Alexandr Petrovich Pischulin, Alexandr Markovich Pochtman, Leonid Mikhailovich Pokrass, Mark Anisimovich Robin, Felix Isaakovich Sheinfain, Igor Sergeevich Slavkin, Pavel Alexandrovich Tesner, Georgy Gavrilovich Zhitnik.
United States Patent |
3,787,038 |
Tesner , et al. |
January 22, 1974 |
REFORMER FOR FIRING REVERBERATORY FURNACE AND METHOD OF OPERATING
SAID REFORMER
Abstract
A reformer for firing a reverberatory furnace comprising a
reaction chamber with a device for incomplete combustion of the
gaseous and liquid hydrocarbon fuel accompanied by the formation of
soot which is supplied into the working space of the furnace for
ensuring a high luminosity of the flame.
Inventors: |
Tesner; Pavel Alexandrovich
(Moscow, SU), Makarov; Konstantin Ivanovich (Moscow,
SU), Ivanov; Alexandr Kornilovich (Moscow,
SU), Robin; Mark Anisimovich (Moscow, SU),
Slavkin; Igor Sergeevich (Moscow, SU), Pischulin;
Alexandr Petrovich (Moscow, SU), Pokrass; Leonid
Mikhailovich (Donetsk, SU), Pochtman; Alexandr
Markovich (Kharkov, SU), Sheinfain; Felix
Isaakovich (Donetsk, SU), Kondratiev; Evgeny
Mikhailovich (Donetsk, SU), Moiseevich; Grigory
Isaevich (Donetsk, SU), Osmaga; Igor Ivanovich
(Donetsk, SU), Zhitnik; Georgy Gavrilovich (Donetsk,
SU) |
Family
ID: |
20449137 |
Appl.
No.: |
05/304,307 |
Filed: |
November 7, 1972 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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103127 |
Dec 31, 1970 |
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Foreign Application Priority Data
Current U.S.
Class: |
266/266; 266/267;
431/351 |
Current CPC
Class: |
F27B
3/00 (20130101); F23D 17/00 (20130101); F27B
3/20 (20130101); C01B 3/36 (20130101); F27B
3/205 (20130101); C21C 5/04 (20130101); C01B
3/22 (20130101); Y02P 10/143 (20151101) |
Current International
Class: |
F23D
17/00 (20060101); C21C 5/00 (20060101); C21C
5/04 (20060101); F27B 3/20 (20060101); F27B
3/00 (20060101); C01B 3/22 (20060101); C01B
3/36 (20060101); C01B 3/00 (20060101); C21c
005/04 () |
Field of
Search: |
;266/24,33,1R ;431/351
;432/20 |
References Cited
[Referenced By]
U.S. Patent Documents
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3554507 |
January 1971 |
Andonley et al. |
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Primary Examiner: Dost; Gerald A.
Attorney, Agent or Firm: John C. Holman et al.
Parent Case Text
This is a divisional, of application Ser. No. 103,127, filed Dec.
31, 1970 and now abandoned.
Claims
What we claim is:
1. A reformer for firing a reverberatory furnace comprising: a
reaction chamber with a cylindrical internal surface communicating
with the working space of said furnace and intended for incomplete
combustion in it of the hydrocarbon fuel, said combustion being
accompanied by the formation of soot to be delivered into the
furnace; a device for incomplete combustion of gaseous hydrocarbon
fuel located in said reaction chamber; said device provided with a
branch pipe supplying gaseous fuel into said chamber and installed
coaxially with the latter, and a branch pipe supplying air into the
same chamber, located tangentially to the internal surface of said
chamber; and a device for incomplete combustion of liquid
hydrocarbon fuel, installed in said chamber near said device for
incomplete combustion of gaseous fuel and provided with a spray
nozzle for the supply of liquid fuel into said reaction
chamber.
2. A reformer according to claim 1 wherein there is an air atomizer
spray nozzle for the supply of liquid fuel, located coaxially
inside said branch pipe for the supply of gaseous fuel.
3. A reformer according to claim 1 wherein the diameter of said
branch pipe for the supply of gaseous fuel into said reaction
chamber is 0.1-0.4 of the inside diameter of this chamber.
4. A reformer according to claim 1 wherein said devices for
incomplete combustion of gaseous and liquid fuels are provided with
known means of independent control of the flow rate of the air,
gaseous and liquid fuels, and of the agent used for atomizing the
liquid fuel.
Description
The present invention relates to the devices for firing
reverberatory furnaces and more particularly it relates to the
reformers for firing open-hearth furnaces and to the method of
their operation involving preliminary preparation of the fuel in
order to ensure a high luminosity of the flame in the furnace.
The present invention can be used most successfully in
reverberatory furnaces and fire-chambers whose efficient operation
requires an intensively radiating and highly luminous flame.
Known in the art are devices for firing reverberatory furnaces with
gaseous fuel, for example, natural gas, wherein the gas is
preliminarily reformed, i.e., incompletely burned which is
accompanied by the formation of soot. Such a device disclosed in
U.S. Pat. No. 3,345,054, and called reformer, has a fire-proof
reaction chamber with a cylindrical internal surface in which
natural gas is reformed under the conditions conductive to a
maximum transformation of carbon contained in gas into soot. The
hot soot-gas mixture obtained in the reformer is mixed with the
non-reformed gas thus producing a fuel mixture. On being introduced
into the furnace, this mixture, containing a required amount of
soot, gives a cone of flame which is characterized by high
luminosity and, in consequence, has a high degree of heat transfer
by radiation to the product being heated. This flame possesses the
requisite rigidity owing to a high velocity of the fuel stream
delivered into the furnace.
For a maximum efficiency of the reforming process, the gaseous fuel
is burned incompletely in the reformer in a rotary turbulent
diffusion flame. For this purpose the gaseous fuel is fed into the
reaction chamber in the form of an axial stream through a
correspondingly set branch pipe of the burner device whereas the
air is delivered through a branch pipe set tangentially to the
cylindrical internal surface of the reaction chamber and installed
in the front part of the reformer, on its side wall. This produces
a rotary diffusion flame in the reformer reaction chamber, this
flame allowing more than 20% of the carbon contained in the gaseous
fuel to be transformed into soot. This is considerably more than
can be obtained with other arrangements for incomplete combustion.
The air consumption in this case is 0.35-0.45 of the stoichiometric
consumption.
However, in such an arrangement said reformer cannot reform liquid
hydrocarbons such as the fuel oil used habitually as a stand-by
fuel or, in absence of natural gas, as the main fuel.
The fuel oil can also be used as an addition to the gaseous fuel
for imparting the required luminosity to the flame, and is fed
directly into the working space of the furnace.
Under these conditions the fuel oil is delivered through spray
nozzles or injectors. In contrast to the gaseous fuel this leads to
the necessity of increasing the coefficient of surplus air and to
unproductive utiliyation of a part of the furnace working space to
prepare the fuel oil for burning. Besides, the soot yield in this
case is not higher than 10 percent of the carbon contained in the
fuel oil. This results in a higher consumption of fuel per ton of
the product.
An object of the present invention resides in eliminating the
aforesaid disadvantages.
The main object of the invention consists in providing a reformer
with such a reaction chamber which would make it possible to use
efficiently both the gaseous and liquid fuel and to produce a
highly luminous flame.
According to the invention, this object is accomplished by
providing the reformer chamber with a device for incomplete
combustion of liquid hydrocarbon fuel, said device being installed
near the device for incomplete combustion of the gaseous fuel and
provided with a spray nozzle for supplying liquid fuel into the
chamber. Such a universal burner device allows reforming both types
of fuel and producing soot in the amount sufficient for the high
luminosity of the flame.
As compared with the known methods of compound firing of furnaces
with gas and fuel oil, preliminary reforming of fuel oil makes it
possible to transform into soot up to 30 percent of the carbon
contained in fuel oil and to produce a highly luminous flame which
requires a smaller amount of surplus air owing to preliminary
preparation of the fuel for combustion, thus reducing the
consumption of fuel.
It is practicable that the liquid fuel should be supplied through
an air atomizer spray nozzle which would be mounted coaxially
inside the branch pipe supplying gaseous fuel in the burner device
for firing gaseous fuel and, simultaneously, coaxially with
relation to the reaction chamber. As it has already been stated
above, the air required for incomplete combustion is delivered
tangentially to the cylindrical internal surface of the reaction
chamber through a specially set branch pipe. This ensures the
optimum conditions for the maximum transformation of the carbon
contained in the fuel into soot, avoiding at the same time the
settling of carbon on the walls of the reaction chamber which
interferes with its normal functioning. Besides, this arrangement
of the burner device for liquid fuel ensures its easy installation,
removal and replacement, when necessary.
It is practicable that the branch pipe supplying gaseous fuel in
the device for burning this fuel should have a diameter equalling
to 0.1 - 0.4 of the diameter of the reformer reaction chamber. This
ensures a rational relation between the velocities of the streams
of air and gaseous fuel and a maximum soot yield. Besides, this
makes it possible to install the liquid fuel spray nozzle coaxially
as it has been described above, without interfering with the
conditions required for independent operation of the reformer on
gaseous fuel.
In the preferable embodiment of the reformer reaction chamber,
according to the invention, it is practicable that the reformer
should incorporate some known devices for independent control of
the flow rate of air, gaseous fuel, liquid fuel and of the agent
which atomizes liquid fuel. This agent may be gas, e.g., natural
gas, or air supplied under the required pressure. The independent
supply of the above-mentioned substances allows the operator at the
control desk to shift the reformer to operation on gaseous or
liquid fuel or on their mixture with the required consumption ratio
of these fuels.
According to the invention, if the furnace is fired with liquid
fuel, the latter is gasified before burning in the reaction chamber
by incomplete combustion accompanied by the formation of soot.
If gaseous fuel is not available, air is used for atomizing liquid
fuel; besides, air can be used for complete combustion of a part of
the liquid fuel outside the reaction chamber in the tunnel burners,
from which the products of complete combustion are delivered
tangentially to the internal surface of the reaction chamber. For
better aerodynamics of the streams in the reaction chamber it is
practicable to install an even number of tunnel burners, for
example two burners opposed diametrically to each other.
A substantial advantage of the present invention lies in reaching a
10 percent economy of fuel as compared with the known methods of
compound firing of furnaces with natural gas and fuel oil.
Described below is a preferable embodiment of the reformer
according to the invention with reference to the accompanying
drawing (which is a schematic longitudinal section through a part
of an open-hearth furnace, including its firing throat, and one of
the reformers communicating with said throat and furnace.
Installed in the firing throat 1 of the furnace 2 is a fire-proof
nozzle 3 of a known design, communicating through a refractory
channel 4 with the reaction chamber 5 of the reformer 6. The nozzle
3 is inclined to the horizontal to suit the required conditions of
product heating in the furnace. The area through the channel in the
nozzle 3 is selected so as to ensure the required velocity of the
fuel mixture flow and to produce a rigid flame. The nozzle 3 is
fitted with a branch pipe 7 for introducing the non-reformed part
of gaseous fuel into the reformed products flowing through the
nozzle.
The reaction chamber 5 of the reformer 6 accommodates devices for
incomplete combustion of gaseous and liquid fuel. The burner device
for gaseous fuel, e.g., natural gas, consists of a gas supply
branch pipe 8 and an air supply branch pipe 9. The branch pipe 8 is
installed coaxially with the reaction chamber 5 while the branch
pipe 9 is set tangentially to the internal cylindrical surface of
the chamber 5. The burner device for liquid fuel, e.g., fuel oil,
comprises an air atomizer spray nozzle 10 of a known design
provided with a pipe 11 for the delivery of the atomizing agent, as
well as the above-mentioned branch pipe 9, a by-pass line 12 with a
shutoff means 13 and a tunnel burner 14 of a known design, adapted
for complete combustion of fuel. The fuel may be fuel oil, natural
gas, coke gas or some other cheap fuel.
The spray nozzle 10 and the pipe 11 are set coaxially inside the
branch pipe 8.
Part of the non-reformed gaseous fuel is supplied to the branch
pipe 7 through the pipeline 15. The air is supplied to the branch
pipe 9 through the pipeline 16 and the by-pass line 12. During
operation of the tunnel burners 14 they are fed with fuel through
the pipeline 17 whereas air is delivered through the pipeline 16.
Part of the gaseous fuel being reformed is delivered to the branch
pipe 8 through the pipeline 18. The reformed liquid fuel is
delivered to the spray nozzle 10 through the pipeline 19. If the
fuel is atomized by natural gas, the latter is supplied to the
branch pipe 11 through the pipeline 20; if the fuel is atomized by
air, the latter is supplied through the pipeline 21.
The pipelines 12, 15, 16, 17, 18, 19, 20 and 21 are fitted with
shut-off means (gate valves), 13, 22, 23, 24, 25, 28, 26 and 27,
respectively.
These means are provided with remote control included into the
atuomatic system (not shown) of controlling the furnace firing and
shifting this firing from one side of the furnace to the other.
If the open-hearth furnace is fired with gaseous fuel, e.g. natural
gas, the shut-off means 23, 24, 26, 27 and 28 must be closed while
the shut-off means 22, 13 and 25 must be open for admitting the
required quantities of gas and air. It is recommended to reform and
supply through the pipeline 18 about 40% of the entire amount of
natural gas used for firing the furnace and to use about 4 m.sup.3
of air per 1 m.sup.3 of natural gas for incomplete combustion in
the reaction chamber. At this air-gas consumption ratio, when gas
is supplied in an axial stream through the branch pipe 8 while air
is supplied in a tangential stream through the branch pipe 9 the
soot yield reaches a maximum. It is practicable that the diameter
of the branch pipe 8 should be 0.1-0.4 of the inside diameter of
the chamber 5.
The hot soot-gas mixture produced in the chamber 5 flows through
the channel 4 into the nozzle 3 where it is mixed with the
non-reformed part of cold gas supplied through the branch pipe 7.
As the non-reformed gas is thus heated, the fuel mixture delivered
into the furnace 2 form the nozzle 3 is better prepared for
complete combustion; as a result, said combustion is accelerated
and proceeds at higher temperatures. All this increases the
radiation heat transfer of the flame.
When the furnace is fired simultaneously with gaseous and liquid
fuels there may be different combinations of the flow rates of
these fuels. In one of the methods it is recommended to reform such
a quantity of fuel oil which corresponds to 20 percent of the total
heat spent for firing the furnace. In this case it is necessary to
open correspondingly the shutoff means 13, 22, 27 and 28 to supply
air for reforming the fuel oil through the by-pass line 12; the
natural gas is fed through pipeline 15 and branch pipe 7 into the
reformed products flowing through the nozzle 3; the natural gas is
also supplied through the pipeline 21 for atomizing the fuel oil
delivered through the pipeline 19.
It is also possible to use other combinations of the consumption
ratio of the gaseous and liquid fuels delivered into the reaction
chamber 5 for the preparation of the hot soot-gas mixture and into
the nozzle 3 for mixing cold gas with said mixture.
Though natural gas can be delivered for reforming into the reaction
chamber 5 simultaneously with fuel oil, it is preferable to employ
such a layout where the fuel oil used for furnace firing is
preliminarily reformed and gasified so that the furnace is supplied
through the nozzle 3 with the products of reforming mixed with
natural gas. Thus, the furnace receives a spray of a fuel mixture
consisting wholly of heated gases containing soot. Subsequent flame
firing of this gaseous fuel mixture proceeds with low surplus air
coefficients characteristic only of the gaseous fuel and,
correspondingly, at high temperatures. This ensures a high
luminosity of the flame and a high heat transfer by radiation.
When natural gas is not available and the furnace is fired with
fuel oil, it is necessary to close the shut-off means 22, 25, 27
and open the shut-off means 26 and 28 for delivering, respectively,
air as an atomizing agent, and liquid fuel for reforming. The
process of reforming can in this case proceed owing to the heat
produced by the combustion of the part of fuel oil delivered into
the chamber 5 through the spray nozzle 10. The air is then
delivered for reforming through the by-pass line 12 and the
shut-off means 13.
The reforming process can also proceed owing to the heat produced
by the combustion of a part of fuel oil in the tunnel burners 14.
It is preferable to have an even number of tunnel burners 14 and
arrange them diametrically opposite to each other for better
aerodynamics of the streams in the chamber 5. In this case said
burners are supplied with the corresponding amounts of fuel oil and
with the quantity of air sufficient for complete combustion of fuel
oil. For this purpose the shut-off means 23 and 24 are opened
through a required angle and the shut-off menas 13 are closed. The
total recommended ratio of the consumption of air and fuel oil
delivered into the reaction chamber is 3 m.sup.3 /kg. This amount
includes the air spent for the atomization of fuel oil. These
conditions ensure the reforming time necessary for obtaining the
sufficient yield of soot as well as the preliminary gasification of
liquid fuel before burning it in the furnace. As a result, the fuel
mixture delivered for flame burning contains combustible hot gases
and a sufficient proportion of soot. Owing to this the flame
combustion proceeds with low coefficients of surplus air which are
characteristic only of gaseous fuel, and at high temperatures. This
also ensures a maximum radiation of the soot contained in the
flame.
While using liquid hydrocarbons as fuel, the invention makes it
possible to subject them to preliminary gasification and transform
them simultaneously into soot in the quantities required for high
luminosity of the flame. The high temperatures produced by the
burning of such prepared fuel increase the radiation of the soot in
the flame and of the flame as a whole which intensifies the heat
transfer and gives at least a 10 percent saving in fuel.
* * * * *